Method for purifying liquid hydrocarbon motor fuels fromsulfur and for further reducing the sulfur dioxide content in exhaust gases up to zero during combustion of the fuels

ABSTRACT

The invention relates to the oil-refining industry, in particular, to methods for purifying a fuel from sulfur-containing compounds, by separating the sulfur-containing modified molecules from the remainder of the fuel molecules on polymer membranes and by activating the fuel purified in the fully-developed cavitation mode prior to the combustion. The reduction of the sulfur content in the fuel is achieved by treating the fuel or a fuel fraction in the fully-developed cavitation mode with addition of a hydrogen peroxide aqueous solution and/or a strong aqueous solution of iron oxides, followed by separating the obtained emulsion into a fuel fraction and a water-paraffin emulsion, followed by separating the fuel fraction on the membranes under the temperature of from 90° C. to 180° C. under atmospheric pressure into a fuel fraction having low sulfur combustion of the purified fuels down to zero by means of activation of the fuels having the low sulfur content.

RELATED APPLICATIONS

This application is a continuation of co-pending U.S. patent applicationSer. No. 16/962,038, filed Jul. 14, 2020, entitled A METHOD FORPURIFYING LIQUID HYDROCARBON MOTOR FUELS FROM SULFUR AND FOR FURTHERREDUCING THE SULFUR DIOXIDE CONTENT IN EXHAUST GASES UP TO ZERO DURINGCOMBUSTION OF THE FUELS, the entire disclosure of which is hereinincorporated by reference.

FIELD OF THE INVENTION

A method for purifying liquid hydrocarbon motor fuels from sulfur andfor further reducing the sulfur dioxide content in exhaust gases up tozero during combustion of the fuels.

BACKGROUND OF THE INVENTION

“A method for purifying oil and oil products from sulfur compounds” thatcomprises treating the oil or oil products with an irrigation liquid,the method characterized in that the oil and oil products arepreliminary treated with a streamer electric discharge, is known. Theliquid is fed for treatment under the pressure of 2-3 MPa at theirrigation path l=(5 . . . 6) a, wherein l is a length of the irrigationpath, a is a distance between nozzles for spraying the irrigation liquid(Ukrainian patent No. 6153 as of 15.04.2005).

A drawback of the method lies in complexity of its implementation. Themethod that is the closest to the claimed invention is “A method forpurifying diesel fuel from sulfur-containing compounds” that comprisesmixing the diesel fuel with chemical substances followed by separationand reduction of the reagents, according to the invention, the dieselfuel is mixed with triethylamine; the obtained mixture is separatedusing polymer membranes by the pervaporation method to form twotechnological streams of the purified diesel fuel and a mixture of thetriethylamine with the removed sulfur-containing compounds, the secondflow is mixed with dimethylsulfoxide and the obtained mixture isseparated by the pervaporation method up!o complete removal oftriethylamine, and the obtained remainder in the form ofdimethylsulfoxide and sulphur compounds is mixed with water, andreagents and the removed sulphur-containing compounds are separated,wherein the separated triethylamine, dimethylsulfoxide and water aredelivered for the repeated use m the closed circuit (Ukrainian patentNo. 75259 as of 15.03.2006).

A drawback of the closest method lies in that the method allowsreduction of the sulfur-containing compounds content in the diesel fuelonly and provides formation of wastes, which must be disinfected orstacked.

SUMMARY OF THE INVENTION

The underlying problem of the invention is to develop a method thatcould enable reduction of the sulfur content in liquid hydrocarbon motorfuels such as petrol, kerosene and diesel fuel up to the level of 20 ppm(parts per million being a measuring unit of a concentration) or lessand reduction of the sulfur dioxide concentration in exhaust gasesduring combustion of these fuels.

DETAILED DESCRIPTION

The stated problem is solved by the method for purifying liquidhydrocarbon motor fuels from sulfur and for further reducing the sulfurdioxide content in exhaust gases up to zero during combustion of thefuels by modifying the sulfur-containing fuel molecules in afully-developed cavitation mode, by separating the sulfur-containingmodified molecules from the remainder of the fuel molecules on thepolymer membranes and by activating the fuel purified up to 20 ppm inthe fully-developed cavitation mode prior to the combustion. What isnovel is that the reduction of the sulfur content in the fuel isachieved by means of treating the fuel or a fuel fraction in thefully-developed cavitation mode with addition of a hydrogen peroxideaqueous solution and/or a strong aqueous solution of iron oxides to thefuels, followed by separating the obtained emulsion into a fuel fractionand a water-paraffin emulsion, followed by separating the fuel fractionon the membranes under the temperature of from 90° to 180° C. under theatmospheric pressure into a fuel fraction having a low sulfur contentand a fuel fraction having an increased sulfur content. Reduction of thesulfur dioxide in the exhaust gases during combustion of the purifiedfuels up to zero by means of activation of the fuels having the lowsulfur content in the fully-developed cavitation mode is performedwithout addition of other chemical substances. Production of a reducedoil-water emulsion from the water-paraffin emulsion and the fuelfraction having the increased sulfur content that increases theefficiency of reduced oils combustion is performed in boiler units.Reduction of the sulfur content in the fuel or fuel fractions isperformed up to the required level of 20 ppm or less. Treatment of theinitial fuel or fuel fraction by the cavitation is performed under thepressure of 1.0-5.0 atm and the temperature of 20° C.-70° C.

A method for purifying liquid hydrocarbon motor fuels from sulfur andfor further reducing the sulfur dioxide content in exhaust gases up tozero is performed as follows. Reduction of the sulfur content in liquidhydrocarbon fuels or fuel fractions, including petrol, kerosene, dieselfuel, up to the required level of 20 ppm or less is achieved by means oftreating the initial fuel or fuel fraction by mechanical, ultrasound orelectrospark cavitation under the pressure of 1.0-5.0 atm and thetemperature of 20° C.-70° C. with addition, to the fuel or fuelfraction, of 1-10 ml of 3%-50% hydrogen peroxide aqueous solution and/ora strong aqueous solution of iron oxides having an own formula in thetotal amount of 0.5%-20% by the fuel volume, while the ratio between thehydrogen peroxide and iron oxides solutions is from 1:2 to 1:10,followed by separating the obtained emulsion into the fuel fraction andthe water-paraffin emulsion, followed by separating the fuel fraction onthe membranes, which are used for extracting the fuel fractions from araw oil, under the temperature of up to 90° C. for purifying petrol, upto 120° C. for purifying kerosene and up to 180° C. for purifying dieselfuel under the atmospheric pressure, into the fuel fraction having a lowsulfur content with the fraction yield of up to 95% by the volume of theincoming fuel, and into the fuel fraction having an increased sulfurcontent (the remainder). The obtained water-paraffin emulsion and thefuel fraction having the increased sulfur content is used for producingthe reduced oil-water emulsion for increasing the efficiency ofcombustion of the reduced oils in boiler units and for reducingemissions of harmful and greenhouse gases. The obtained fuel fractionhaving the sulfur content of 20 ppm or less is treated by the mechanicalcavitation without addition of other substances that allows reduction ofthe sulfur level in the exhaust gases of the internal combustion enginesand boiler units up to zero in case an activated fuel is used duringfive days after treatment.

Reduction of the sulfur content m the motor fuels, including petrol,kerosene, diesel fuel, is achieved by means of: partial targetedoxidation of the sulfur-containing compounds, which are comprised in thefuels, by the hydrogen peroxide, bonding of the sulfur with the iron,destroying the sulfur compounds with the hydrocarbon molecules, whichare permeable for membranes being used, and formation of the sulfurcompounds in the fuel, which do not penetrate through the membranes inthe process of the cavitation treatment of the mixture; partial bondingof the sulfur with—the iron in the process of the cavitation treatmentof the mixture; destroying the sulfur compounds with the hydrocarbonmolecules, which are permeable for the membranes being used, andformation of the sulfur compounds, which do not penetrate through themembranes, during the cavitation treatment with addition of the hydrogenperoxide and iron oxides in the fuel; conversion of thesulfur-containing hydrocarbon compounds into the sulfur compounds withoxygen and/or with iron in the process of the cavitation treatment ofthe mixture without addition of chemical substances; reduction of thesulfur content in the exhaust gases up to zero due to the treatment ofthe preliminary purified fuel by the mechanical cavitation and consumingthe fuel during 14 days after the fuel treatment.

The claimed method reduced the sulfur content in liquid hydrocarbonfuels or fuel fractions, including petrol, kerosene, diesel fuel, up tothe required level of 20 ppm or less, and reduced the sulfur dioxidecontent in the exhaust gases up to zero under the condition of consumingthe fuel during five days after fuel activation. The reduced oil-wateremulsion for increasing the efficiency of reduced oils combustion in theboiler units is produced from the wastes formed in the treatmentprocess.

What is claimed is:
 1. A hydrocarbon fuel product manufactured by aprocess for purifying liquid hydrocarbon motor fuels by reduction of asulfur content and for further reducing a sulfur dioxide content inexhaust gases down to zero during combustion of the fuels by means ofchemical transformation of sulfur-containing molecules of the fuels in afully-developed cavitation mode, physical separation of modifiedsulfur-containing molecules from the remainder of the molecules onmembranes followed by activation of the fuels in the fully-developedcavitation mode prior to the combustion, the process comprising:treating the fuel or fuel fraction in the fully-developed cavitationmode with addition, to the fuel, of a hydrogen peroxide aqueous solutionin the amount of 1-10 ml of the hydrogen peroxide per 1 liter of thefuel and/or an aqueous solution of iron oxides in the amount of 0.5%-20%of the fuel volume, followed by; separating an obtained emulsion into afuel fraction and a water-paraffin emulsion, and followed by; separatingthe fuel fraction on the membranes under a temperature of from 90° C. to180° C. under the atmospheric pressure into a fuel fraction having a lowsulfur content of up to 20 ppm and into a fuel fraction having anincreased sulfur content, including reduction of the sulfur dioxidecontent own to zero in the exhaust gases by means of activation prior tothe combustion of the fuel fraction having the low sulfur content in thefully-developed cavitation mode without addition of other chemicalsubstances, production of a reduced oil-water emulsion from thewaterparaffin emulsion and the fuel fraction having the increased sulfurcontent for combustion in boiler units.
 2. The fuel product of claim 1,wherein wastes, which must be disinfected or stacked, are not formedduring the process of purification of the fuels from the sulfur.
 3. Thefuel product of claim 1 wherein the fuel comprises at least one ofpetrol, kerosene and diesel.
 4. The fuel product of claim 1, furthercomprising, separating the sulfur-containing modified molecules from theremainder of the fuel molecules on polymer membranes and activating thefuel purified up to 20 ppm fuel.
 5. The fuel product of claim 4, whereina level of 20 ppm or less is achieved by initially treating the fuel orfuel fraction by mechanical, ultrasound or electrospark cavitation undera pressure of 1.0-5.0 atm and a temperature of 20° C.-70° C. withaddition, to the fuel or fuel fraction, of 1-10 ml of 3%-50% hydrogenperoxide aqueous solution and/or a strong aqueous solution of ironoxides having an own formula in the total amount of 0.5%-20% by the fuelvolume, while the ratio between the hydrogen peroxide and iron oxidessolutions is from 1:2 to 1:10, followed by separating the obtainedemulsion into the fuel fraction and the water-paraffin emulsion,followed by separating the fuel fraction on the polymer membranes, at atemperature of up (a) to 90° C. for purifying petrol, (b) up to 120° C.for purifying kerosene and (c) up to 180° C. for purifying diesel fuelat atmospheric pressure.